Catalyst comprising a metal substrate

ABSTRACT

A catalyst comprising a metal or alloy substrate, an oxidation resistant coating applied to the substrate, the coating comprising aluminum metal powder in a ceramic binder, a high surface area catalytic washcoat over the oxidation resistant coating and a catalytically active material, e.g. a platinum group metal, associated with the washcoat.

This application is a continuation of U.S. application Ser. No. 876,565,filed Feb. 10, 1978, now U.S. Pat. No. 4,196,099.

FIELD OF THE INVENTION

The invention is concerned with certain advantageous improvements insupported catalysts intended for use at elevated temperatures. Morespecifically the invention relates to catalysts which are supported onmetal substrates. These catalysts are capable of a wide variety of usesat elevated temperatures as will be hereinafter evident. However, aparticularly important area of use is in the treatment of automobileexhaust gases or the like to remove air pollutants therein.

It is a well known fact that in recent years, due to environmentalrestrictions, it has become necessary to catalytically convert varioustypes of noxious exhaust gases into non-toxic or less toxic gases beforethey are discharged into the atmosphere. For example, it has now becomeconventional to pass the exhaust gases from an automobile engine orsimilar type of internal combustion engine through a catalytic convertersystem before discharge into the atmosphere. These exhaust gasesnormally contain large amounts of NO_(x), hydrocarbons and carbonmonoxide. However, passage through the catalytic converter reduces theNO_(x) and/or oxidizes the hydrocarbons and carbon monoxide to carbondioxide and water.

The catalytic converter used for automobile exhaust gas may comprise ahoneycomb structure including substrate which is capable of withstandingthe high temperature of the exhaust gas and which has been coated with acatalytically active platinum group metal or metals, e.g. platinum orplatinum/rhodium alloy. To increase surface area and to improve adhesionof the catalytic coating to the substrate, a high surface area catalytic"washcoat", usually comprising alumina, is initially applied to thesubstrate followed by deposition of the platinum group metal (see, forexample, U.S. Pat. Nos. 2,580,806; 2,664,340; 2,742,437; 2,742,434;2,921,035; 3,565,830; 3,920,583 and British Pat. No. 690,825).

The substrate is most usually a ceramic or refractory which can beprepared into a honeycomb or the like having a high surface area.However, there have also been a variety of proposals to use differenttypes of metals or alloys which are oxidation resistant and otherwisecapable of withstanding high temperatures as the substrate. In thisconnection, see, for example, U.S. Pat. No. 3,920,583 which describes acatalyst comprising a substrate made of an alloy or iron, chromium,aluminum and yttrium (commonly called "Fecralloy"), an alumina washcoatand a platinum group metal catalytic surface. According to U.S. Pat. No.3,920,583, the substrate should be subjected to a heat treatment todevelop an aluminum oxide surface which serves to key the washcoat andcatalytic surface thereto.

U.S. Pat. No. 3,867,313 also describes a catalyst comprising a heatresistant nickel-free alloy consisting essentially of aluminum, chromiumand iron (e.g. "Kanthal" alloys) as the substrate with a noble metalcatalytic coating thereon. The catalyst of this patent is an all-metalone and does not apparently include a washcoat. However, the patent doesillustrate another prior effort to use a metal alloy as a catalystsubstrate.

Other patents which describe various types of catalysts comprising ametal substrate include the following:

U.S. Pat. Nos.

3,231,520

3,437,605

3,712,856

3,719,739

3,773,894

3,891,575

3,907,708

3,923,696

3,953,176

3,957,692

3,966,646

3,992,330

British Pat. No. 470,894

Where the catalyst is to be used at high temperature in the presence ofair or oxygen as, for example, in the case of automobile exhaustcontrol, the metal substrate, if used, is normally fabricated fromexpensive high temperature oxidation resistant metals or alloys (e.g.Fecralloy or Kanthal as mentioned above). It is not, for example,possible to effectively use conventional stainless steel or the like asthe substrate for auto exhaust catalysts, at least in the absence ofsome kind of special treatment, since the stainless steel is incapableof withstanding the high temperatures which are involved. On the otherhand, special alloys such as Fecralloy and Kanthal are expensive and thesupply thereof is not always adequate. Additionally, in the case ofFecralloy, the heat treatment required to develop the oxide "keying"surface adds to the time and cost involved in preparing the catalyst.There is, therefore, a real need in the art to provide a simple andconvenient way of using less expensive metals and alloys which normallydo not possess adequate high temperature oxidation resistance, such asstainless steel, as substrates for catalysts to be used at hightemperature, e.g. auto exhaust gas catalysts. The principal object ofthe invention is, therefore, to provide novel catalysts based onstainless steel or the like which are capable of use at elevatedtemperature. Other objects will also be apparent from the followingdescription of the invention.

SUMMARY OF THE INVENTION

Broadly stated, the invention contemplates rendering a metal whichnormally would be unsuitable as the substrate for a catalyst to be usedat high temperature (e.g. above 1200° F.), suitable for such use byfirst coating the metal with a thin high temperature oxidation resistantlayer, as defined below, prior to conventional washcoating with aluminaor other material and application of the catalytically active material,e.g. platinum group metal.

The high temperature oxidation resistant layer is obtained by applyingto the metal substrate an aqueous coating composition which is curableat a temperature below 500° F. and may comprise dissolved phosphate,preferably aluminum phosphate; dissolved dichromate or molybdate; solidparticulate material such as powdered metal, powdered alloys andrefractory metal oxides and a modifier which permits curing intowater-insoluble form at a temperature below 500° F. Advantageously theparticulate material is aluminum metal powder and the modifier is anamine, preferably an alkanol amine such as diethanolamine.

While a number of coating compositions of the type described above arecommercially available and suitable for use herein, a particularlypreferred composition is "Alseal-500" which is available from Coatingsfor Industry, Incorporated, Philadelphia, Pa. The product comprises adispersion of aluminum metal powder (5 micron size) in an aqueoussolution of a chromium salt (CrO₃) and a ceramic binder such as aluminumphosphate.

it is understood that Alseal-500 and generally equivalent coatingcompositions are described in Belgian Pat. No. 825,180, the subjectmatter of which is incorporated herein by reference. Alseal-500 isdescribed in available trade literature as a high temperature, corrosionand oxidation resistant coating material for ferrous alloys whichcontains aluminum powder in an organo-inorganic ceramic binder and hasthe unique characteristic of being curable at temperatures as low as250° F. when heated at that temperature for 30 minutes. This is lowcompared to other types of cermet ceramic/inorganic coatings and meansthat the coatings can be applied and cured at temperatures which wouldnot adversely affect the metal substrate. A further feature ofAlseal-500 is that the corrosion and oxidation protection affordedthereby is excellent at high temperatures, e.g. 1200° F.

Details as to the preparation of "Alseal-500" and possible compositionalvariations therein are not described herein since these are given inBelgian Pat. No. 825,180. However, it is noted that preferredcompositions for the organic-inorganic binder, before addition of thealuminum metal particles or equivalent, will generally fall within thefollowing ranges:

    ______________________________________                                                        Preferred Amounts, GMS                                        ______________________________________                                        dissolved phosphate                                                                             about 1 to about 6                                          dissolved dichromate                                                                            about 0.15 to about 3.5                                     and/or molybdate                                                              metal ion         about 1 to about 6                                          amine             about 0.02 to about 0.3                                     ______________________________________                                    

Usually from about 20 to about 2000 g/l of aluminum metal powder orother particulate material will be added to the binder to give thecoating composition as used.

The following illustrates one way of preparing an aluminum metal/ceramiccoating composition for use herein to give the desired oxidationresistant coating:

An aluminum phosphate/CrO₃ solution was prepared by combining 300 g ofhydrated alumina (Al₂ O₃.H₂ O) with 558 ml of 75% phosphoric acid andthereafter high speed mixing. After standing overnight the solution wasdecanted from the insoluble Al(OH)₃ which had settled to the bottom. Theresulting solution was diluted with water to yield a 60% by weightaluminum phosphate solution. To 100 ml of this solution, 12 g of (CrO₃)was added.

An aqueous organic-inorganic binding solution is then prepared by mixingtogether the following:

    ______________________________________                                        H.sub.2 O               25     ml                                             aluminum phosphate and  100    ml                                             CrO.sub.3 solution as prepared                                                above                                                                         (HOCH.sub.2 CH.sub.2).sub.2 NH                                                                        3      g                                              ______________________________________                                    

100 ml of the thus prepared binding solution and 90 g of aluminum metalpowder (-400 mesh) are then combined to give a coating compositionsuitable for use herein.

Other coating compositions containing dissolved phosphate, dissolveddichromate or molybdate, and solid particulate material which may beused herein, preferably with appropriate modification to lower thecuring temperature, are disclosed in a publication entitled"Investigation of Aluminum Phosphate Coatings for Thermal Insulation ofAir Frames", by Eubanks and Moore, National Aeronautics and SpaceAdministration (NASA Technical Note D-106, 1959) and U.S. Pat. No.3,248,251 to Allen. Appropriate modifications of these compositions tolower the curing temperature are described in U.S. Pat. Nos. 3,248,250and 3,248,249. According to U.S. Pat. No. 3,248,250, the curingtemperature is lowered by adding an alkali metal silicate while U.S.Pat. No. 3,248,249 proposes the addition of a solid particulate materialhaving a grain size on the order of 0.1 micron or finer to lower thecuring temperature.

The metal substrate used herein may be made of any metal (includingalloys) which can be fabricated into the desired form (e.g. honeycomb)but which normally would not be sufficiently heat and/or oxidationresistant at high temperature to be suitable for use as a catalystsubstrate. Typically suitable are the stainless steels of the 400series, e.g. stainless steel 420 which is free of nickel and alumuniumbut has a relatively high chromium content (e.g. 13% Cr, balanceessentially iron). Normally stainless steel 420 could not be used as asubstrate in the usual way (i.e. by application of washcoat and platinumgroup metal) as an automobile exhaust gas catalyst becauase the alloycould not effectively withstand the high temperature of the exhaust gasand exotherms of several hundred degrees during periods of hydrocarbonrich operation. However, application of the oxidation resistant layer,e.g. aluminum/ceramic coating according to the invention, makes itpossible to satisfactorily use the alloy as the substrate for an exhaustgas catalyst.

The ceramic coating, e.g. Alseal-500 or the equivalent, may be appliedin any convenient fashion, e.g. by spraying to the desired thickness.The coating may be dried by heating at 150°-200° F. for at least 15minutes (no maximum time) followed by curing at 250°-350° F. for atleast 30 minutes, e.g. 4-6 hours (no maximum time). If desired, thecoating may be given a further post-firing at about 1025° F. for 60minutes or more (no maximum time) although this is not necessary. Singleor plural coatings may be used. Normally the coating or coatings in thefinished catalyst will have a thickness of about 0.5 to about 4 mils,preferably about 1-2 mils. Where multiple coats are applied, curingshould be effected after each coating.

The oxidation resistant ceramic coating may be applied to the substratebefore or after the substrate is shaped into the desired form. Forexample, the coating may be applied directly to flat and corrugatedstrips of metal before rolling to form a honeycomb structure or thehoneycomb may be made first followed by application of the oxidationresistant coating.

After application of the oxidation resistant coating, a conventionalhigh surface area refractory oxide washcoat, preferably alumina, isapplied in the usual fashion followed by drying and calcining andapplication of the platinum group metal or metals, all as conventionallyemployed in the preparation of exhaust gas catalysts (See, for example,U.S. Pat. No. 3,920,583).

The importance of using the aluminum/ceramic coating according to theinvention is shown by the fact that after 420 stainless steel is coatedwith "Alseal-500" and fired at 1100° F., it shows no undesirable effectswhatsoever when held overnight at 2000° F. In contrast, 420 stainlesssteel held overnight at 2000° F. without being coated with "Alseal" isvery badly damaged.

The FIGURE discloses a graph of the conversion results of carbonmonoxide and hydrocarbons with respect to time.

The invention is illustrated, but not limited, by the following example:

EXAMPLE 1

Two automobile exhaust catalysts A and B were prepared to test theirability to convert hydrocarbons and carbon monoxide in automobileexhaust gas. The catalysts were made by wrapping alternating sheets offlat and corrugated metal around a 1/4" mandrel to form cylindricalhoneycomb substrates about 3" long and 2" diameter. In one case(catalyst A), representative of the invention, the metal sheetsconsisted of stainless steel 420 while in the other (catalyst B), thesheets consisted of Fecralloy. The Fecralloy substrate had been heattreated at high temperature to form an aluminum oxide "keying" surface.Catalyst B was completed by dipping the heat treated Fecralloy cylinderin a conventional alumina washcoat, followed by drying, calcining andthen depositing platinum group metals (2 parts Pt, 1 part Pd) on thewashcoat in conventional fashion.

Catalyst A was prepared by uniformly spraying the stainless steel 420cylinder with Alseal-500. The thus coated cylinder was dried at 200° F.and cured at 350° F. for 30 minutes. The Alseal-500 coating was about1-1.5 mil thick after drying and curing. The cylinder was then given aone hour post firing at 1025° F. Washcoat and platinum group metal werethen applied exactly as in the case of the Fecralloy substrate.

Catalysts A and B were then connected at one end to the exhaust of astandard 8-cylinder Ford engine. The other end of each catalyst wasconnected to an analyzer for determining the percent conversion ofhydrocarbons (HC) and carbon monoxide (CO) in the exhaust gas. Thepercent conversions at various times are shown in the following table:

                                      TABLE I                                     __________________________________________________________________________    Hours Operation                                                                        3.5                                                                             25                                                                              70                                                                              140                                                                              190                                                                              250                                                                              300                                                                              350                                                                              400                                                                              440                                                                              480                                                                              510                                    __________________________________________________________________________    Catalyst A                                                                    (stainless                                                                    steel                                                                         substrate)                                                                    % Conversions                                                                 HC       79                                                                              78                                                                              76                                                                              71 68 67 64 61 55 57 56 47                                     CO       96                                                                              95                                                                              96                                                                              96 95 94 93 88 86 83 76 71                                     Catalyst B                                                                    (Fecralloy                                                                    substrate)                                                                    HC       79                                                                              78                                                                              75                                                                              70 70 71 69 65 58 58 52 46                                     CO       95                                                                              92                                                                              93                                                                              91 92 93 93 90 87 82 75 69                                     __________________________________________________________________________

The catalysts were cleaned and blown out after 510 hours operation toremove particulate or foreign material, e.g. rust and possibly manganesedioxide from gasoline additives, which tended to clog and otherwisereduce the catalyst efficiency. The catalysts were thereafter againconnected up and the percent HC and CO determined with the followingresults:

                  TABLE II                                                        ______________________________________                                        Hours Operation                                                                             535      560      585    620                                    ______________________________________                                        % Conversion                                                                  Catalyst A                                                                    HC            61       56       61     58                                     CO            88       88       86     85                                     Catalyst B                                                                    HC            61       60       65     60                                     CO            92       93       90     90                                     ______________________________________                                    

The results shown in Tables I and II are also illustrated graphically inthe attached FIG. 1.

As will be evident from Tables I and II and the drawing, Catalysts A andB are essentially equivalent in terms of HC and CO conversion.Comparison of the test samples also showed them to be in substantiallyidentical condition after the tests. There was no indication ofdeterioration, corrosion or rusting on either sample. Catalyst Aappeared to have a slightly thicker wash coating than the Catalyst B(Fecralloy) unit but this was apparently due to the slightly roughersurface resulting from the Alseal-500 coating. Thus, the use of theAlseal has the advantage of giving an increased washcoat thicknesswithout requiring any change in the washcoat properties. There was alsoa very tight surface bond between the metal substrate and the washcoatas a result of the Alseal-500 coating. Apparently, the strong bondbetween the metal substrate and ceramic coating is due to aluminumdiffusion and the formation of intermetallic compounds.

EXAMPLE 2

In a further series of tests eight catalysts were made up and tested asautomobile exhaust catalysts as in Example 1. The results are shownbelow in terms of percent hydrocarbon (HC) and carbon monoxide (CO)conversion after the indicated hours of operation:

    __________________________________________________________________________                50    100   150   200   250   300                                             Hrs.  Hrs.  Hrs.  Hrs.  Hrs.  Hrs.                                Catalyst                                                                           Substrate                                                                            HC CO HC CO HC CO HC CO HC CO HC CO                               __________________________________________________________________________    1    Fecralloy                                                                            72 94 65 95 61 92 65 90 46 83 53 85                               2    Fecralloy                                                                            68 95 68 94 64 92 65 92 53 85 53 86                               3    Fecralloy                                                                            75 95 70 94 64 92 68 94 49 83 54 83                               4    Fecralloy                                                                            74 96 71 95 67 93 67 93 52 87 54 88                               5    Fecralloy                                                                            69 95 66 92 61 89 61 87 53 83 47 83                                    420 Stainless                                                            6    Steel                                                                         No Alseal                                                                            60 80 63 82 63 85 64 84 66 85.5                                                                             54 85                               7    420 Stainless                                                                 Steel  62 92 60 86 59 88 64 88 68 85 63 86                                    with Alseal                                                                   420 Stainless                                                            8    Steel  73 94 69 93 68 92 66 92 70 90 62 91                                    with Alseal                                                              __________________________________________________________________________

The "Fecralloy" substrate used in catalysts 1-4 was prepared bysubjecting the alloy to oxidation at 1200° C. for 1 hour to develop aprotective oxide coating thereon. In the case of Catalyst 5, theFecralloy substrate was coated with a Ce-Sol. In catalysts 6-8, thestainless steel was heated to 850° F. and after application of the"Alseal" in the case of Nos. 7 and 8, the substrate was further heatedat 1000° F.

The tabulated results show that the "Alseal" catalysts according to theinvention retained their effectiveness over the 300 hour test period.

Various modifications may be made in the invention as described in theforegoing. Thus, while the catalyst has been described in connectionwith the treatment of automobile exhaust gas for the control ofhydrocarbon and carbon monoxide pollutants, the catalyst may be used forother purposes. For example, the present catalyst may be used inprocesses involving catalytic (flameless) combustion, ammonia oxidation,high temperature catalytic oxidations other than automobile exhaustcontrol (e.g. fume and/or odor abatement), high temperature catalytichydrogenation including methanation, Fischer Tropsch reaction, coalliquefaction, nitric oxide abatement, and the like. More specifically,methanation and Fischer Tropsch reactions can be carried out bycontacting CO and H₂ gas, with or without added steam, with the presentcatalyst. Nitric acid may be prepared by contacting ammonia and oxygen,e.g. air, with the catalyst under otherwise conventional conditions.Catalytic combustion may be carried out by contacting the appropriatefuel/air (or oxygen) mixture with the catalyst. Additionally, it isnoted that, while the invention is of particulate importance for usewith stainless steel and/or other metals or alloys which are notnormally oxidation resistant at high temperatures, the invention mayalso be used in applications involving alloys which have hightemperature oxidation resistance, e.g. the Kanthal or Fecralloy typealloy, where, for example, a particularly high level of bonding may bedesired between the catalytic material and the substrate. Accordingly,the scope of the invention is defined in the following claims wherein:

We claim:
 1. A supported catalyst suitable for use at a temperatureabove 1200° F. consisting essentially of a metal or alloy substratewhich itself is not heat or oxidation resistant at a temperature above1200° F.; a heat-cured oxidation resistant coating applied to saidsubstrate, said coating being applied as an aqueous coating compositionwhich is curable into water-insoluble oxidation resistant form byheating and which consists essentially of a dispersion of aluminum metalpowder in an aqueous chromium-containing/aluminum phosphate bindercomposition; a high surface area refractory oxide washcoat over saidoxidation resistant coating and a catalytically active platinum groupmetal deposited on said washcoat.
 2. A catalyst according to claim 1wherein the substrate is a stainless steel.
 3. A catalyst according toclaim 2 wherein the substrate is stainless steel
 420. 4. A catalystaccording to claim 1 wherein the catalytically active material comprisesone or more platinum group metals or combination of PGM's with othercatalytic materials.
 5. In a supported catalyst which is suitable foruse at elevated temperatures comprising a metal or alloy substrate whichitself is not heat or oxidation resistant at the temperature of use andwhich is used to support a catalytically active platinum group metalsupported on said substrate, the improvement which comprises aheat-cured oxidation resistant coating applied to said substrate betweenthe substrate and the platinum group metal to protect the substrate,said coating being applied as an aqueous coating composition which iscurable into water-insoluble oxidation resistant form by heating andwhich consists essentially of a dispersion of aluminum metal powder inan aqueous chromium-containing/aluminum phosphate binder.